聚乙烯醇辐照交联共聚物渗透气化分离膜

研究了聚乙烯醇(PVA)与丙烯酰胺丙烯酸钠共聚物(PcoAANa)的辐照交联共聚物膜用于水-乙醇混合物的渗透气化分离,随着PcoAANa在共聚物中的含量由0%上升到35%,透量及分离系数同时增大,膜材料对混合物中水及乙醇的选择性溶解,对渗透气化过程起重大影响。求出了水、乙醇及其混合物的表现透过活化能.水,乙醇和混合物的平均扩散系数在水含量为40%时出现极大值。     

邻苯二甲酸二辛酯增塑聚氯乙烯膜的富氧分离性能

本文研究了DOP含量为0—70%(重量)的增塑PVC膜的透氧性能,指出DOP含量为50%左右的PVC膜要比纯PVC膜的气体透过率提高二个数量级,约为1.7×10^-9cm³。cm/cm²·s·cmHg,氧氮分离系数为4。DOP含量为20%的PVC膜有较高的氧氮分离系数,约为6.9。     

二氧化硅陶瓷管上silicalite-1分子筛膜的制备及其分离性能

利用原位水热合成在二氧化硅陶瓷管上制备出高性能的silicalite-1分子筛膜。使用溶液填充方法后,膜的平均透量提高了25％,60℃分离乙醇／水混合物时膜的透量和分离系数分别为0.99kg／（m^2·h）和73。实验结果表明,二氧化硅陶瓷管上制备的分子筛膜具有很高的热稳定性和制备重复性,平均透量和分离系数的相对标准偏差（R.S.D.）分别为9.6％和5.6％。这一结果显示,二氧化硅载体更适合制备高性能silicalite-1分子筛膜。     

高性能silicalite-1分子筛膜的合成及其渗透汽化性能

采用两步原位水热合成法在新型多孔二氧化硅陶瓷管上成功合成出高性能的silicalite-1分子筛膜, 60℃时乙醇/水的分离系数达到了84, 透量达到了0.56 kg/(m²·h). 利用扫描电子显微镜(SEM)对其进行了表征; 研究了不同合成条件对silicalite-1分子筛膜乙醇/水分离性能的影响. 实验结果表明, 在相同的合成条件下, 利用甘油-水的混合溶液填充陶瓷管载体后, 可以提高膜的平均透量约26%. 多次活化结果表明, 二氧化硅载体上合成的分子筛膜以活化速率4℃/min升温到400℃并活化5 h, 仍然保持原来的分离选择性. 由此说明, 二氧化硅载体更适合高性能silicalite-1分子筛膜的制备.     

Ind2ZrCln(OC6H3-3,5-Me2)2-n/一氯二乙基铝催化乙烯齐聚的研究

合成了 Ind2 Zr(OC6 H3- 3,5 - Me2 ) 2 (A)、 Ind2 Zr Cl(OC6 H3- 3,5 - Me2 ) (B)和 Ind2 Zr Cl2 (C) 3个化合物 ,并在不同反应温度、陈化温度、反应时间等条件下 ,分别考察了每个化合物与 Et2 Al Cl所组成的催化体系对乙烯齐聚活性和选择性的影响 .在相同条件下 ,催化剂活性顺序为 A>B>C;在最佳反应条件下 ,Ind2 Zr(OC6 H3- 3,5 - Me2 ) 2的催化活性为 195 1g齐聚物 / (g Zr· h) ,C4～ 1 0 烯烃选择性为 95 .0 % ,1- C4～ 1 0 =(直链 α-烯烃 )选择性为 85 .5 % .     

LTV—PSF富氧膜的复合机理研究

用不同种类和浓度的极性有机物水溶液(醇-水溶液、羧酸-水溶液、多官能团有机物-水溶液)以及四种类型(阳离子、阴离子、两性、非离子)表面活性剂水溶液处理聚砜支撑膜改变其表面化学特性,改善硅橡胶汽油溶液在其表面的铺展性能;用两次浸泡减少涂层过程中硅橡胶汽油溶液向支撑膜内的渗透程度,使LTV-PSF复合膜的透量获得较大幅度的提高。同时考察了聚砜支撑膜结构因素的影响。     

酯化交联聚乙烯醇膜用于渗透气化法分离EtoH／H2O的研究

合成了一系列磷酸和二元羧酸酯化交联改性的聚乙烯醇(PVA)膜,研究了它们用于水-乙醇混合液的渗透气化分离规律。磷酸改性的PVA膜具有较大的通量,当料液浓度为50%时,通量可达1200g/m~2·hr.,分离系数α_(H_2O/EtOH)=10。丙二酸改性PVA膜在料液浓度为50%时,通量可达800g/m~2·hr.,且α_(H_2O/EtOH)=18。并作了这两种膜的通量和分离系数随料液浓度的变化曲线。草酸交联的PVA膜具有较高的分离系数,但通量很小。求出了水、乙醇及总的表现渗透活化能。     

海洋放线菌Streptomyces sp. V5产生的一个新的八元环内酯

海洋放线菌Streptomyces sp. V5分离自南中国海红树根部土壤, 从其培养液分离获得一个新的八元环内酯octalactin C (A), 以及四个已知化合物2-甲基-3-呋喃甲酸(B)、环(脯-亮)二肽(C)、环(丙-缬)二肽(D)和尿嘧啶(E). 通过完整的波谱数据解析了它们的结构.     

SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜研究

通过在磺化聚醚醚酮(SPEEK,DS=61.68%)中分别混入酚酞型聚醚砜(PES-C)、磺化酚酞型聚醚砜(SPES-C,DS=53.7%)制备出SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜.结果表明,共混的两种聚合物之间均具有较好的相容性.PES-C、SPES-C的混入能有效降低膜的溶胀及甲醇透过,且随着共混量的增加,这种作用越趋明显.纯SPEEK膜在75℃左右溶解,而SPEEK/PES-C(30wt%)、SPEEK/SPES-C(30wt%)共混膜在80℃时溶胀度仅为22.5%、26.32%.在室温至80℃范围内,纯SPEEK及共混膜的甲醇透过系数都在10-7cm2.s-1数量级上,远小于Nafion115膜.在饱和湿度下,温度大于90℃时,SPEEK/PES-C(20wt%)共混膜电导率超过Nafion115膜;温度大于110℃时,SPEEK/SPES-C(30wt%)共混膜电导率与Nafion115膜相当,达到0.11S.cm-1.高电导率,低透醇系数以及明显提高了的可使用温度表明该类共混膜有望在DMFC中使用.     

SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜研究

通过在磺化聚醚醚酮(SPEEK,DS=61.68%)中分别混入酚酞型聚醚砜(PES-C)、磺化酚酞型聚醚砜(SPES-C,DS=53.7%)制备出SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜.结果表明,共混的两种聚合物之间均具有较好的相容性.PES-C、SPES-C的混入能有效降低膜的溶胀及甲醇透过,且随着共混量的增加,这种作用越趋明显.纯SPEEK膜在75℃左右溶解,而SPEEK/PES-C(30 wt%)、SPEEK/SPES-C(30 wt%)共混膜在80℃时溶胀度仅为22.5%、26.32%.在室温至80℃范围内,纯SPEEK及共混膜的甲醇透过系数都在10-7 cm2·s-1数量级上,远小于Nation[R]115膜.在饱和湿度下,温度大于90℃时,SPEEK/PES-C(20 wt%)共混膜电导率超过Nation[R]115膜;温度大于110℃时,SPEEK/SPES-C(30 wt%)共混膜电导率与Nafion[R]115膜相当,达到0.11 S·cm-1.高电导率,低透醇系数以及明显提高了的可使用温度表明该类共混膜有望在DMFC中使用.     

高活性载体Ziegler-Natta催化剂的研究

<正> 用反应法(MgCl_2/ROH/TiCl_4)合成MgCl_2载体Ziegler-Natta催化剂已被聚烯焊工业越来越广泛的接受。这不仅是因为这种催化剂体系具有高活性,用于α-烯烃聚合能得到高等规度的聚合物;而且比用研磨法制备催化剂易于控制操作条件,合成这种催化剂的关键步骤是醇溶解MgCl_2,再在低温下与TiCl_4反应。放出HCl和形成Ti(OR)Cl_3的同时,MgCl_2再次从溶液中沉淀出来而得到很好的载体。过去,曾从不同     

丙烷在无机膜反应器中的芳构化

研究了在固定床反应器和膜反应器中的丙烷芳构化，考察了ＨＺＳＭ－５担载的Ｇａ和Ｐｔ－Ｇａ催化剂对反应的影响。结果表明，采用无机膜反应器可以提高丙烷芳构化选择性，从而提高芳烃收率达１０％以上。在膜反应器中，低碳烷烃选择性降低，烯烃选择性增强。固定床相比，膜反应器在低温时对芳构化反应的促进作用最为显著，但是随着温度升高，其促进作用减弱。     

PhCH=P[MeNCH(2)CH(2)](3)N: a novel ylide for quantitative E selectivity in the Wittig reaction

PhCH=P[MeNCH(2)CH(2)](3)N (1), a semi-stabilized ylide prepared from the commercially available nonionic base P[MeNCH(2)CH(2)](3)N, reacts with aldehydes to give alkenes in high yield with quantitative E selectivity. In contrast with other ylides, this E selectivity is maintained despite changes in the metal ion of the ionic base used to deprotonate 1, temperature, and solvent polarity. In conjunction with structural parameters gained from the X-ray molecular structure of 1, the pathway to E selectivity in these reactions is rationalized by the Vedejs model of Wittig reaction stereochemistry.     

Boltorn-modified polyimide gas separation membranes

This paper describes the preparation, characterization and permeation properties of polyimide BTDA-AAPTMI (Matrimid 5218) and co-polyimide BTDA-TDI/MDI (P84) dense polymer films containing aliphatic hyperbranched polyesters, Boltorn (H40). The H40 are dispersed in the polymers at various concentrations.

For Matrimid–H40 1.0 wt% membrane the nitrogen permeability increases but with significant loss in selectivity, while at higher H40 concentrations (5.0 and 10.0 wt%) the permeability becomes lower than of the pure polymer and the selectivity generally stays constant. The dispersion of various concentrations of H40 (1.0, 5.0 and 10.0 wt%) in P84 membranes decreases gas permeability in comparison to pure P84, while the selectivity generally stays constant.     

Dehydration of tetrafluoropropanol (TFP) by pervaporation via novel PBI/BTDA-TDI/MDI co-polyimide (P84) dual-layer hollow fiber membranes

A novel PBI/P84 co-polyimide dual-layer hollow fiber membrane has been specifically fabricated through the dry-jet wet phase inversion process, for the first time, for the dehydration pervaporation of tetrafluoropropanol (TFP). Polybenzimidazole (PBI) was chosen as the outer selective layer because of its superior hydrophilic nature and excellent solvent-resistance together with robust thermal stability, while P84 co-polyimide was employed as the inner supporting layer because of its good solvent-resistance and thermal stability. The PBI/P84 membrane exhibits superior water selectivity and relatively high permeation flux. At 60 °C, the PBI/P84 dual-layer hollow fiber membrane shows a permeation flux of 332 g/(m² h) and a separation factor of 1990 for a feed solution containing of 85 wt% TFP. The preferential water sorption and the significant diffusivity difference between TFP and water are the main causes of high separation factor. However, an increase in feed temperature will greatly increase the permeation flux but seriously decrease the water selectivity. The activation energy data verify that water can preferentially permeate the PBI membrane due to the strong water affinity of PBI and a much smaller molecular size of water.     

Colloidal stability of electrostatically stabilized sol particles.

The colloid stability of ferric hydroxide sol has been investigated at three different HCl concentrations. The total HCl concentration in the sols was A>B>C, the amount of HCl adsorbed was A=B>C. The parameters which characterize the stability (flocculation value, gelation concentration, repeptizability) are related to the amount of adsorbed HCl, because this property governs the hydrophility of the sols. In contrast, the peptizability of powders after drying the sols depends on the total concentration of HCl in the system. The hydrochloric acid impedes the condensation of surface groups to Fe–O–Fe bonds.From water vapor adsorption and heat of immersion data the hydration potential barrier is constructed which is comparable to the barrier according to the DLVO theory The differences and anomalies in the stability of sols are interpreted as differences in the hydrophility of samples.     

混合导体透氧膜反应器中甲烷部分氧化反应的催化行为(英文)

应用组成为Ba0.5Sr0.5Co0.8Fe0.2O3-(的钙钛矿型混合导体陶瓷膜制成膜反应器。该膜在进行氧分离的同时具有活化甲烷氧化偶联的催化功能。随着温度升高和膜的富氧端氧分压的增大,透氧量有所增加。在空气、氦气的氧分压梯度下,850(C,膜厚度为1.5 mm时,JO2可达到1.2 mL/(cm3(min)。同时在800(C~900(C温度范围内,该膜对于甲烷转化为乙烷和乙烯一般只具有0.5%~3.5%的低转化率,而选择性可达40%~70%。在反应尾气中发现了大量的未反应的分子氧,说明过量的氧与甲烷未经催化反应的气相反应导致了C2的选择性相对较低。OCM膜反应模式情况下的透氧量与空气、氦气梯度情况下的透氧量相比只有微小增加,这与POM膜反应模式情况下透氧量大量增加显著不同。     

Poly(vinyl alcohol)/poly(methyl methacrylate) blend membranes for pervaporation separation of water + isopropanol and water + 1,4-dioxane mixtures

Pervaporation (PV) separation of water + isopropanol and water + 1,4-dioxane mixtures has been attempted using the blend membranes of poly(vinyl alcohol) (PVA) with 5 wt.% of poly(methyl methacrylate) (PMMA). These results have been compared with the plain PVA membrane. Both plain PVA and PVA/PMMA blend membranes have been crosslinked with glutaraldehyde in an acidic medium. The membranes were characterized by differential scanning calorimetry and universal testing machine. Pervaporation separation experiments have been performed at 30 °C for 10, 15, 20, 30 and 40 wt.% of feed water mixtures containing isopropanol as well as 1,4-dioxane. PVA/PMMA blend membrane has shown a selectivity of 400 for 10 wt.% of water in water + isopropanol feed, while for water + 1,4-dioxane feed mixture, membrane selectivity to water was 104 at 30 °C. For both the feed mixtures, selectivity for the blend membrane was higher than that observed for plain PVA membrane, but flux of the blend membrane was lower than that observed for the plain PVA membrane. Membranes of this study are able to remove as much as 98 wt.% of water from the feed mixtures of water + isopropanol, while 92 wt.% of water was removed from water + 1,4-dioxane feed mixtures at 30 °C. Flux of water increased for both the feed mixtures, while the selectivity decreased at higher feed water concentrations. The same trends were observed at 40 and 50 °C for 10, 15 and 20 wt.% of water mixtures containing isopropanol as well as 1,4-dioxane feed mixtures, which also covered their azeotropic composition ranges. Membrane performance was studied by calculating flux (J_p), selectivity (), pervaporation separation index (PSI) and enrichment factor (β). Permeation flux followed the Arrhenius trend over the range of temperatures investigated. It was found that by introducing a hydrophobic PMMA polymer into a hydrophilic PVA, the selectivity increased dramatically, while flux decreased compared to plain PVA, due to a loss in PVA chain relaxation.     

基于季戊四醇的三代硅碳烷液晶树状物研究

用发散法合成了季戊四醇-四烯丙基醚为核、周边含硝基偶氮苯介晶基元(M-NO₂)端基的新型三代硅碳烷液晶树状物PCSi-3G-NO₂, 并利用元素分析、红外光谱(IR)、核磁共振(NMR)、偏光显微镜(POM)、差示扫描量热法(DSC)和X射线衍射(XRD)进行表征. PCSi-3G-NO₂显示胆甾相和近晶S_E相, 其液晶相行为是K57S_E115I100Ch80S_E53K. 而对应的介晶基元M-NO₂显示向列相, 二者在熔点、清亮点和液晶态温区等方面差别较大.     

电子传输材料噻二唑衍生物的密度泛函研究

用密度泛函B3LYP方法对7种3-(3'-吡啶基)-6-芳基-1,2,4-三唑并[3,4-b]-1,3,4-噻二唑分子进行全优化, 所有化合物都是平面分子. 计算了分子的垂直电子亲和势(VEA)、绝热电子亲和势(AEA)、分子内重组能以及绝对硬度等相关能量, 结果显示化合物的HOMO 与LUMO能级可通过连接不同取代基进行调节, 变化幅度为0.346～1.10 eV. 分子内重组能证实3-(4'-氰基-3'-吡啶基)-6-芳基-1,2,4-三唑并[3,4-b]-1,3,4-噻二唑是很有前途的电子传输材料, 不同取代基所对应的化合物分子内重组能也不同. 绝对硬度数据与分子内重组能都表明, 化合物E, G难于传输电子. 用TDDFT方法计算了化合物A, B和C的吸收光谱, 与实验值相比, 最大吸收峰的差值在3～10 nm之间.